US20120325468A1 - Fluid migration shut-off - Google Patents
Fluid migration shut-off Download PDFInfo
- Publication number
- US20120325468A1 US20120325468A1 US13/530,369 US201213530369A US2012325468A1 US 20120325468 A1 US20120325468 A1 US 20120325468A1 US 201213530369 A US201213530369 A US 201213530369A US 2012325468 A1 US2012325468 A1 US 2012325468A1
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- Prior art keywords
- fluid
- compartment
- line
- trap
- assembly
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
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- 239000012530 fluid Substances 0.000 title claims abstract description 176
- 230000005012 migration Effects 0.000 title claims abstract description 17
- 238000013508 migration Methods 0.000 title claims abstract description 17
- 238000004891 communication Methods 0.000 claims abstract description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 239000012528 membrane Substances 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 5
- 239000003345 natural gas Substances 0.000 claims description 5
- 238000011144 upstream manufacturing Methods 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 description 31
- 238000004519 manufacturing process Methods 0.000 description 12
- 238000002347 injection Methods 0.000 description 9
- 239000007924 injection Substances 0.000 description 9
- 230000004888 barrier function Effects 0.000 description 6
- -1 dewaxers Substances 0.000 description 3
- 238000000429 assembly Methods 0.000 description 1
- 230000000712 assembly Effects 0.000 description 1
- 230000003190 augmentative effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000037361 pathway Effects 0.000 description 1
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002455 scale inhibitor Substances 0.000 description 1
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- 239000004094 surface-active agent Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
Images
Classifications
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/34—Arrangements for separating materials produced by the well
- E21B43/38—Arrangements for separating materials produced by the well in the well
Definitions
- Check valves are included to prevent natural gas and other fluids from undesirably migrating up through the chemical injection lines.
- the performance of these check valves is not always adequate to prevent all fluid migration, particularly under static conditions (no chemical being injected) or while chemicals are being injected at lower rates.
- Problems with check valves may include debris caught in the valves, wear or degradation of the valves over time, problematic installations, etc. Accordingly, advances in preventing fluid migration are always well received by the industry.
- a downhole assembly including a line operatively arranged to carry a first fluid, and a trap arranged in fluid communication with the line, the trap operatively arranged to enable the first fluid to flow in a first direction, while capturing a second fluid in a compartment, thereby preventing migration of the second fluid through the line in a second direction opposite to the first direction.
- a method of operating a downhole system including injecting a first fluid through a line in a first direction and capturing a second fluid in a compartment connected in fluid communication with the line, the second fluid traveling through the line in a second direction opposite to the first direction.
- FIG. 1 is a schematic view of a fluid migration shut-off assembly
- FIG. 2 is a schematic view of a fluid trap of the fluid migration shut-off assembly of FIG. 1 ;
- FIG. 3 is a schematic view of a debris catch of the fluid migration shut-off assembly of FIG. 1 ;
- FIG. 4 is a schematic view of an alternate embodiment for a debris catch as disclosed herein;
- FIG. 5 is a schematic view of an alternate embodiment for a debris catch as disclosed herein;
- FIG. 6 is a schematic view of an alternate embodiment for a fluid trap as disclosed herein;
- FIG. 7 is a schematic view of an alternate embodiment for a fluid trap as disclosed herein.
- FIG. 8 is a schematic view of an alternate embodiment for a debris catch and fluid trap as disclosed herein.
- the assembly 10 is included along a chemical injection line 12 .
- the chemical injection line 12 is arranged in a borehole spanning between a surface in which the borehole is made (e.g., a surface of the Earth) and production tubing in the borehole for enabling operators at the surface to inject chemicals or the like downhole, such as demulsifiers, clarifiers, corrosion inhibitors, scale inhibitors, dewaxers, surfactants, etc., for aiding in production.
- the assembly 10 is arranged to prevent the migration of natural gas or other fluids, up the injection line 12 to the surface.
- the assembly 10 includes a trap 14 and a debris catch 16 .
- the chemical injection line 12 comprises several sections, namely, lines 12 a , 12 b , and 12 c .
- the line 12 a is connected between an inlet 18 of the debris catch 16 and the surface
- the line 12 b is connected between an outlet 20 of the debris catch and an inlet 22 of the trap 14
- the line 12 c is connected between an outlet 24 of the fluid trap and the production tubing.
- the lines 12 a , 12 b , and 12 c act to reverse the direction of flow of the line 12 as it travels from the surface to the production tubing in order to trap, catch, or otherwise contain debris, gas, or other fluids undesirably located in the line 12 . the injection line 12 to the surface.
- one or more check valves are included between the production tubing and the line 12 c , it is probable that some degree of leakage, weeping, etc. will occur and that gas or other low-density fluids will escape from the production tubing and migrate up the line 12 toward the surface.
- a difference in densities between a first fluid being injected downhole (e.g., a liquid chemical) and a second fluid flowing through the production tubing (e.g., natural gas) will result in the second fluid migrating up the line 12 . That is, the more dense fluid will exert a buoyancy force on the less dense fluid equal to the weight of the more dense fluid that is displaced by the less dense fluid, causing the less dense fluid to rise and separate.
- the examples herein may refer to the low-density fluid as a gas, e.g., natural gas, and the high density fluid as a liquid, e.g., a liquid chemical, although it is to be appreciated that any other relatively low-density fluid could migrate up any other relatively high-density fluid or vice-versa.
- a gas e.g., natural gas
- a liquid e.g., a liquid chemical
- An arrow 26 in FIG. 2 designates a direction of flow of the chemical fluid through the line 12 .
- a low-density fluid 28 has flowed up the line 12 c , through the outlet 24 and into the trap 14 , where the low-density fluid 28 has gathered in a compartment 30 of the trap 14 .
- the term “low-density” is used for convenience and is made with respect to the density of the injected fluid in the line 12 , e.g., a chemical liquid or the like.
- the low-density fluid 28 has become trapped in the trap 14 because a net buoyancy force created by the difference in densities caused the low-density fluid 28 to float into the compartment 30 on top of the injected chemical fluid.
- the more dense fluid is free to flow along the path 26 from the inlet 22 to the outlet 24 , while the low-density fluid 28 remains trapped in the compartment 30 .
- the inlet 22 is positioned opposite from, away from, or is otherwise secluded from the low-density fluid 28 in the compartment 30 in order to prevent the low-density fluid 28 from reaching the inlet 22 of the trap 14 , where back flow, vaporization, etc. of chemical fluid may enable the low density fluid to reach the inlet 18 of the debris catch 16 , and continue unobstructed up the line 12 a to the surface.
- a plurality of assemblies 10 could be installed in series along the line 12 to further prevent migration.
- a check valve is used to create a chemical fluid barrier for preventing the migration of the low-density fluid 28 further up the line 12 .
- a variety of methods for secluding or isolating the inlet 22 from the low-density fluid 28 is possible, although a simple embodiment is to set a vertical separation between the compartment 30 and the inlet 22 . Under normal conditions, a buoyancy force has only a vertically upward component, by creating a vertical separation between the inlet 22 and the compartment 30 , the low-density fluid can not escape down the line 12 b and/or up the line 12 a without first escaping the compartment 30 , such as by filling its entire volume. Even if the low-density fluid 28 fills the entire volume of the compartment, as discussed in more detail below, a check valve can be incorporated to create a fluid barrier for preventing the migration of the low-density fluid up the line 12 .
- debris or the like from the surface may drop down the injection line 12 and collect in the bends of the line, impeding chemical fluid flow or clogging the line 12 all together.
- the debris catch 16 can be utilized in some embodiments in addition to the trap 14 in order to catch debris 32 and contain the debris 32 at a containment area 34 of the debris catch 16 .
- the chemical fluid as again represented by the arrow 26 , will not be trapped like the more dense debris, but will instead flow from the line 12 a into the line 12 b via the inlet 18 and the outlet 20 of the debris catch 16 .
- the catch 16 thus works similarly to the trap 14 , but also oppositely, in that the relatively higher density of the debris 32 causes the debris 32 to sink under the flow 26 of the fluid, instead of a relatively lower density causing the low-density fluid 28 to float atop the flow 26 of injected fluid.
- debris 28 could comprise solids, relatively high-density fluids (with respect to the injected fluid), or mixtures thereof.
- a check valve 36 is included at the inlet 18 of the debris catch 16 .
- the check valve 36 could alternatively be included at the outlet 20 , along the lines 12 a or 12 b , or at some other suitable location to prevent back flow.
- the check valve 36 not only prevents the back flow of injected fluid, but it also acts as yet another means for preventing the migration of low-density fluid, e.g., the low-density fluid 28 , to the surface.
- improved performance may be achievable by creating a vertical separation between the inlet 22 and the inlet 18 , for example as shown by the line 12 b in the Figures.
- By arranging the inlet 22 higher than the inlet 18 and positioning the check valve 36 upstream of the trap 14 it is possible to prevent the back flow of chemical fluid, and therefore migration of low-density fluid, down the line 12 b or up out of the catch 16 . That is, as the low-density fluid 28 gathers in the trap 14 , any remaining chemical fluid may be forced out of the trap 14 down the line 12 c by the gathering low-density fluid.
- the chemical fluid in the line 12 b will not be able to back flow, and will therefore act as a barrier for preventing the low-density fluid 28 from flowing into the catch 16 or to the surface.
- the buoyancy force is directed in a vertically upward direction, the low-density fluid will not be able to flow down the line 12 b absent the back flow of chemical fluid.
- check valve 36 is subjected to virtually only the chemical fluid, and is thus much less likely to experience the same failure rates as check valves downhole that are subjected to the low-density fluids in the production tubing (e.g., hydrocarbons) and any other debris (e.g., fine sand grains) carried by the low-density fluid.
- the low-density fluids in the production tubing e.g., hydrocarbons
- any other debris e.g., fine sand grains
- FIGS. 4-8 Several variations of components of the assembly 10 are shown in FIGS. 4-8 . It is to be noted that some elements in FIGS. 4-8 are labeled with prime, double prime, or triple prime symbols because, while they generally resemble the corresponding elements having the same base reference numeral (i.e., those numerals without the prime symbols), at least one difference is noted herein between the elements labeled with prime, double prime, or triple prime symbols and their corresponding elements in the previously described embodiments. All other descriptions of the corresponding elements apply also to the elements identified with prime, double prime, or triple prime symbols.
- a debris catch 16 ′ is shown (generally resembling the catch 16 ), having a baffle 38 and a funnel 40 .
- the baffle 38 is included to act as a barrier for any debris, e.g., directing the debris 32 to fall into the containment area 34 of the catch 16 ′.
- the funnel 40 also acts to direct the debris into the containment area 34 , where it is held. This arrangement is advantageous, for example, in the event the fluid in the catch 16 ′ becomes agitated, the baffle 38 and funnel 40 will act as barriers to direct the debris 32 and keep the debris from escaping.
- the baffle 38 or the funnel 40 could be made from a mesh or screen, for example, so that the fluid is able to flow therethrough, but the debris 32 is not.
- the baffle 38 is formed as, or otherwise replaced by, a screen or filter spanning across the debris catch in order to isolate the outlet from the inlet of the catch. It is to be appreciated that in other embodiments the baffle 38 and the funnel 40 could be used separately.
- a debris catch 16 ′′ is shown (generally resembling the debris catch 16 ), having a cyclone 42 therein.
- An inlet 18 ′′ is directed horizontally into the catch 16 ′′ (as opposed to the inlet 18 , which is directed vertically into the catch 16 ) in order to cause the fluid to circulate in the cyclone 42 for depositing the debris 32 in the containment area 34 of the catch 16 ′′.
- An output 20 ′′ may be positioned at the center of the catch 16 ′′ to assist in the flow of fluid out of the cyclone 42 .
- the catch 16 ′′ provides an embodiment in which the fluid is free to flow out of the outlet of the catch while the debris is directed to and then held in the containment area.
- FIG. 6 One example of an embodiment in which the low-density fluid is removable is illustrated in FIG. 6 .
- a trap 14 ′ is shown (generally resembling the trap 14 ), having a membrane 44 and a low-density fluid outlet 46 to a line 48 located in a vented compartment 30 ′.
- the membrane 44 is included in this embodiment is permeable to the low-density fluid 28 , but substantially impermeable to the injected chemical fluid. This enables the low-density fluid to collect above the membrane 44 in the compartment 30 ′, while the chemical fluid flows normally from the line 12 b to the line 12 c .
- This embodiment is particularly useful if the low-density fluid is a gas and the injected chemical fluid is a liquid in that the membrane 44 may be, for example, a polytetrafluoroethylene filter or the like.
- the low-density fluid outlet 46 is provided so that the low-density fluid 28 collected in the trap 14 ′ can be removed from the trap 14 ′.
- the low-density fluid could be vented or pumped back down into the production tubing, into an area of the production tubing located up-hole, or to some other desired location.
- the trap could be periodically flushed at an elevated fluid flow rate to force the low-density fluid back down into the production tubing.
- the fluid used to flush the low-density fluid could be selected such that the solubility of the low-density fluid in the injected chemical fluid is high, in order to assist in the removal of the low-density fluid from the trap.
- a venturi pump, air aspirator, or other mechanism could be installed in, e.g., the line 48 , in order to draw the low-density fluid out of the trap and pump the low-density fluid back into the production tubing or to some other desired location.
- FIG. 7 Several more aspects of the invention are appreciable in view of the embodiment of FIG. 7 , namely, a trap 14 ′′.
- the trap 14 ′′ is horizontally orientated, including a horizontal inlet 22 ′′ and a horizontal outlet 24 ′′ (resembling the inlet 22 and outlet 24 , respectively, but being horizontally oriented) and is thus installable in a horizontal section of a borehole.
- This embodiment still utilizes the behavior of the low-density fluid rising as a result of its relatively lower density.
- the low-density fluid 28 rises into a compartment 30 ′′ (resembling compartment 30 , but partially formed by a wall 50 and being horizontally oriented), as designated by arrows 52 .
- a compartment 30 ′′ (resembling compartment 30 , but partially formed by a wall 50 and being horizontally oriented), as designated by arrows 52 .
- the low-density fluid 28 will rise into the compartment 30 ′′ and become trapped well before the low-density fluid reaches the inlet 22 ′′, with the wall 50 secluding or isolating the inlet 22 ′′ from the trapped low-density fluid 28 .
- the flow of injected fluid as designated again by the arrow 26 , will simply flow under the trapped low-density fluid 28 and out the outlet 24 ′′.
- the inlets of the trap and/or debris catch can be located at other locations as well.
- the inlets and outlets of various embodiments could be placed in the top, bottom, side, or any other desired location of the catch or trap, so long as a compartment is formed that secludes the inlet (with respect to the direction of flow of the injected fluid) of the debris catch and/or fluid trap from the trapped low-density fluid.
- FIG. 8 illustrates a combined unit 54 including both a low-density fluid trap 14 ′ and a debris catch 16 ′′′ in a single, integrated assembly.
- the line section 12 b would be unnecessary, as the trap and catch are integrated together.
- the illustrated embodiment of the combined unit 54 includes a baffle 60 , a funnel 62 for the trap 14 ′, and a funnel 64 for the catch 16 ′′′, for directing the low-density fluid 28 into the compartment 30 and the debris 32 into the containment area 34 , respectively.
- the baffle 60 and the funnel 62 act to seclude or isolate a combined inlet 66 from the low-density fluid 28 as the low-density fluid 28 migrates up the line 12 c and enters the combined unit 54 via a combined outlet 68 , while the baffle 60 and the funnel 64 act to contain the debris so it does not clog the injection line 12 .
- the flow of fluid as again represented by the arrows 26 , flows essentially unimpeded around the baffle 60 and between the funnels 62 and 64 from the inlet 66 to the outlet 68 . It is to be appreciated that that features shown could be removed, or replaced or augmented by other features, such as an outlet for venting the compartment, a permeable membrane, screens, a venturi pump, etc.
- the combined unit 54 could be made rotationally symmetrical, as shown, so that it can be installed in either direction. It is also to be appreciated that, as shown in FIG. 8 , the combined inlet 66 could be located lower than the combined outlet 68 and a check valve 70 could be included at the inlet 66 or in the line 12 a for creating a chemical fluid barrier, similar to the use of the check valve 36 described above, that prevents the migration of the low-density fluid 28 out of the compartment 30 . That is, as the low-density fluid gathers in the unit 54 , chemical fluid in the unit 54 will drain down the line 12 c , to reach the level of the outlet 68 . Once the chemical fluid drops down to the level of the outlet 68 , no more chemical fluid will be forced out the outlet 68 and the check valve 70 will prevent back flow out the inlet 66 , thereby holding the low-density fluid 28 in the unit 54 .
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Abstract
A downhole assembly, including a line operatively arranged to carry a first fluid, and a trap arranged in fluid communication with the line, the trap operatively arranged to enable the first fluid to flow in a first direction, while capturing a second fluid in a compartment, thereby preventing migration of the second fluid through the line in a second direction opposite to the first direction.
Description
- This application claims the benefit of an earlier filing date from U.S. Provisional Application Ser. No. 61/500,995 filed Jun. 24, 2011, the entire disclosure of which is incorporated herein by reference.
- Chemical injection systems are used in the downhole drilling and completions industry. Check valves are included to prevent natural gas and other fluids from undesirably migrating up through the chemical injection lines. The performance of these check valves is not always adequate to prevent all fluid migration, particularly under static conditions (no chemical being injected) or while chemicals are being injected at lower rates. Problems with check valves may include debris caught in the valves, wear or degradation of the valves over time, problematic installations, etc. Accordingly, advances in preventing fluid migration are always well received by the industry.
- A downhole assembly, including a line operatively arranged to carry a first fluid, and a trap arranged in fluid communication with the line, the trap operatively arranged to enable the first fluid to flow in a first direction, while capturing a second fluid in a compartment, thereby preventing migration of the second fluid through the line in a second direction opposite to the first direction.
- A method of operating a downhole system, including injecting a first fluid through a line in a first direction and capturing a second fluid in a compartment connected in fluid communication with the line, the second fluid traveling through the line in a second direction opposite to the first direction.
- The following descriptions should not be considered limiting in any way. With reference to the accompanying drawings, like elements are numbered alike:
-
FIG. 1 is a schematic view of a fluid migration shut-off assembly; -
FIG. 2 is a schematic view of a fluid trap of the fluid migration shut-off assembly ofFIG. 1 ; -
FIG. 3 is a schematic view of a debris catch of the fluid migration shut-off assembly ofFIG. 1 ; -
FIG. 4 is a schematic view of an alternate embodiment for a debris catch as disclosed herein; -
FIG. 5 is a schematic view of an alternate embodiment for a debris catch as disclosed herein; -
FIG. 6 is a schematic view of an alternate embodiment for a fluid trap as disclosed herein; -
FIG. 7 is a schematic view of an alternate embodiment for a fluid trap as disclosed herein; and -
FIG. 8 is a schematic view of an alternate embodiment for a debris catch and fluid trap as disclosed herein. - A detailed description of one or more embodiments of the disclosed apparatus and method are presented herein by way of exemplification and not limitation with reference to the Figures.
- Referring now to
FIG. 1 , anassembly 10 is shown. Theassembly 10 is included along achemical injection line 12. Thechemical injection line 12 is arranged in a borehole spanning between a surface in which the borehole is made (e.g., a surface of the Earth) and production tubing in the borehole for enabling operators at the surface to inject chemicals or the like downhole, such as demulsifiers, clarifiers, corrosion inhibitors, scale inhibitors, dewaxers, surfactants, etc., for aiding in production. Theassembly 10 is arranged to prevent the migration of natural gas or other fluids, up theinjection line 12 to the surface. - The
assembly 10 includes atrap 14 and adebris catch 16. Thechemical injection line 12 comprises several sections, namely, 12 a, 12 b, and 12 c. Thelines line 12 a is connected between aninlet 18 of thedebris catch 16 and the surface, theline 12 b is connected between anoutlet 20 of the debris catch and aninlet 22 of thetrap 14, and theline 12 c is connected between anoutlet 24 of the fluid trap and the production tubing. As will be better appreciated in view of the below, the 12 a, 12 b, and 12 c act to reverse the direction of flow of thelines line 12 as it travels from the surface to the production tubing in order to trap, catch, or otherwise contain debris, gas, or other fluids undesirably located in theline 12. theinjection line 12 to the surface. - Although one or more check valves are included between the production tubing and the
line 12 c, it is probable that some degree of leakage, weeping, etc. will occur and that gas or other low-density fluids will escape from the production tubing and migrate up theline 12 toward the surface. For example, a difference in densities between a first fluid being injected downhole (e.g., a liquid chemical) and a second fluid flowing through the production tubing (e.g., natural gas) will result in the second fluid migrating up theline 12. That is, the more dense fluid will exert a buoyancy force on the less dense fluid equal to the weight of the more dense fluid that is displaced by the less dense fluid, causing the less dense fluid to rise and separate. The examples herein may refer to the low-density fluid as a gas, e.g., natural gas, and the high density fluid as a liquid, e.g., a liquid chemical, although it is to be appreciated that any other relatively low-density fluid could migrate up any other relatively high-density fluid or vice-versa. - An
arrow 26 inFIG. 2 designates a direction of flow of the chemical fluid through theline 12. In this embodiment, a low-density fluid 28 has flowed up theline 12 c, through theoutlet 24 and into thetrap 14, where the low-density fluid 28 has gathered in acompartment 30 of thetrap 14. The term “low-density” is used for convenience and is made with respect to the density of the injected fluid in theline 12, e.g., a chemical liquid or the like. Again, it is to be appreciated that the low-density fluid 28 has become trapped in thetrap 14 because a net buoyancy force created by the difference in densities caused the low-density fluid 28 to float into thecompartment 30 on top of the injected chemical fluid. The more dense fluid is free to flow along thepath 26 from theinlet 22 to theoutlet 24, while the low-density fluid 28 remains trapped in thecompartment 30. - The
inlet 22 is positioned opposite from, away from, or is otherwise secluded from the low-density fluid 28 in thecompartment 30 in order to prevent the low-density fluid 28 from reaching theinlet 22 of thetrap 14, where back flow, vaporization, etc. of chemical fluid may enable the low density fluid to reach theinlet 18 of thedebris catch 16, and continue unobstructed up theline 12 a to the surface. In some embodiments, a plurality ofassemblies 10 could be installed in series along theline 12 to further prevent migration. In another embodiment described in more detail below, a check valve is used to create a chemical fluid barrier for preventing the migration of the low-density fluid 28 further up theline 12. - A variety of methods for secluding or isolating the
inlet 22 from the low-density fluid 28 is possible, although a simple embodiment is to set a vertical separation between thecompartment 30 and theinlet 22. Under normal conditions, a buoyancy force has only a vertically upward component, by creating a vertical separation between theinlet 22 and thecompartment 30, the low-density fluid can not escape down theline 12 b and/or up theline 12 a without first escaping thecompartment 30, such as by filling its entire volume. Even if the low-density fluid 28 fills the entire volume of the compartment, as discussed in more detail below, a check valve can be incorporated to create a fluid barrier for preventing the migration of the low-density fluid up theline 12. - It is noted that debris or the like from the surface may drop down the
injection line 12 and collect in the bends of the line, impeding chemical fluid flow or clogging theline 12 all together. As a result, thedebris catch 16 can be utilized in some embodiments in addition to thetrap 14 in order to catchdebris 32 and contain thedebris 32 at acontainment area 34 of thedebris catch 16. The chemical fluid, as again represented by thearrow 26, will not be trapped like the more dense debris, but will instead flow from theline 12 a into theline 12 b via theinlet 18 and theoutlet 20 of thedebris catch 16. Thecatch 16 thus works similarly to thetrap 14, but also oppositely, in that the relatively higher density of thedebris 32 causes thedebris 32 to sink under theflow 26 of the fluid, instead of a relatively lower density causing the low-density fluid 28 to float atop theflow 26 of injected fluid. It should be appreciated thatdebris 28 could comprise solids, relatively high-density fluids (with respect to the injected fluid), or mixtures thereof. In order to prevent the back flow of chemical fluid, acheck valve 36 is included at theinlet 18 of thedebris catch 16. Thecheck valve 36 could alternatively be included at theoutlet 20, along the 12 a or 12 b, or at some other suitable location to prevent back flow. Advantageously, thelines check valve 36 not only prevents the back flow of injected fluid, but it also acts as yet another means for preventing the migration of low-density fluid, e.g., the low-density fluid 28, to the surface. - More than simply providing a vertical separation between the
compartment 30 and theinlet 22, improved performance may be achievable by creating a vertical separation between theinlet 22 and theinlet 18, for example as shown by theline 12 b in the Figures. By arranging theinlet 22 higher than theinlet 18 and positioning thecheck valve 36 upstream of thetrap 14, it is possible to prevent the back flow of chemical fluid, and therefore migration of low-density fluid, down theline 12 b or up out of thecatch 16. That is, as the low-density fluid 28 gathers in thetrap 14, any remaining chemical fluid may be forced out of thetrap 14 down theline 12 c by the gathering low-density fluid. However, due to thecheck 36, the chemical fluid in theline 12 b will not be able to back flow, and will therefore act as a barrier for preventing the low-density fluid 28 from flowing into thecatch 16 or to the surface. Alternatively stated, since the buoyancy force is directed in a vertically upward direction, the low-density fluid will not be able to flow down theline 12 b absent the back flow of chemical fluid. It is noted that thecheck valve 36 is subjected to virtually only the chemical fluid, and is thus much less likely to experience the same failure rates as check valves downhole that are subjected to the low-density fluids in the production tubing (e.g., hydrocarbons) and any other debris (e.g., fine sand grains) carried by the low-density fluid. - Several variations of components of the
assembly 10 are shown inFIGS. 4-8 . It is to be noted that some elements inFIGS. 4-8 are labeled with prime, double prime, or triple prime symbols because, while they generally resemble the corresponding elements having the same base reference numeral (i.e., those numerals without the prime symbols), at least one difference is noted herein between the elements labeled with prime, double prime, or triple prime symbols and their corresponding elements in the previously described embodiments. All other descriptions of the corresponding elements apply also to the elements identified with prime, double prime, or triple prime symbols. - In
FIG. 4 , adebris catch 16′ is shown (generally resembling the catch 16), having a baffle 38 and afunnel 40. The baffle 38 is included to act as a barrier for any debris, e.g., directing thedebris 32 to fall into thecontainment area 34 of thecatch 16′. Thefunnel 40 also acts to direct the debris into thecontainment area 34, where it is held. This arrangement is advantageous, for example, in the event the fluid in thecatch 16′ becomes agitated, the baffle 38 and funnel 40 will act as barriers to direct thedebris 32 and keep the debris from escaping. The baffle 38 or thefunnel 40 could be made from a mesh or screen, for example, so that the fluid is able to flow therethrough, but thedebris 32 is not. In one embodiment, the baffle 38 is formed as, or otherwise replaced by, a screen or filter spanning across the debris catch in order to isolate the outlet from the inlet of the catch. It is to be appreciated that in other embodiments the baffle 38 and thefunnel 40 could be used separately. - In
FIG. 5 , adebris catch 16″ is shown (generally resembling the debris catch 16), having acyclone 42 therein. Aninlet 18″ is directed horizontally into thecatch 16″ (as opposed to theinlet 18, which is directed vertically into the catch 16) in order to cause the fluid to circulate in thecyclone 42 for depositing thedebris 32 in thecontainment area 34 of thecatch 16″. Anoutput 20″ may be positioned at the center of thecatch 16″ to assist in the flow of fluid out of thecyclone 42. Thus, thecatch 16″ provides an embodiment in which the fluid is free to flow out of the outlet of the catch while the debris is directed to and then held in the containment area. - If enough low-density fluid rises into the compartment of the fluid trap, it is possible for the low-density fluid to fill the entire volume of the compartment of the fluid trap, which could result in the low-density fluid seeping out the inlet of the fluid trap, through the debris catch, and up the line to the surface. Accordingly, it may be desirable to include a means for at least periodically removing the low-density fluid from the fluid trap. One example of an embodiment in which the low-density fluid is removable is illustrated in
FIG. 6 . In this embodiment, atrap 14′ is shown (generally resembling the trap 14), having amembrane 44 and a low-density fluid outlet 46 to aline 48 located in a ventedcompartment 30′. Themembrane 44 is included in this embodiment is permeable to the low-density fluid 28, but substantially impermeable to the injected chemical fluid. This enables the low-density fluid to collect above themembrane 44 in thecompartment 30′, while the chemical fluid flows normally from theline 12 b to theline 12 c. This embodiment is particularly useful if the low-density fluid is a gas and the injected chemical fluid is a liquid in that themembrane 44 may be, for example, a polytetrafluoroethylene filter or the like. In this embodiment, the low-density fluid outlet 46 is provided so that the low-density fluid 28 collected in thetrap 14′ can be removed from thetrap 14′. For example, the low-density fluid could be vented or pumped back down into the production tubing, into an area of the production tubing located up-hole, or to some other desired location. - As another example of a method for removing low-density fluid from the trap, the trap could be periodically flushed at an elevated fluid flow rate to force the low-density fluid back down into the production tubing. The fluid used to flush the low-density fluid could be selected such that the solubility of the low-density fluid in the injected chemical fluid is high, in order to assist in the removal of the low-density fluid from the trap. In another embodiment, a venturi pump, air aspirator, or other mechanism could be installed in, e.g., the
line 48, in order to draw the low-density fluid out of the trap and pump the low-density fluid back into the production tubing or to some other desired location. - Several more aspects of the invention are appreciable in view of the embodiment of
FIG. 7 , namely, atrap 14″. Thetrap 14″ is horizontally orientated, including ahorizontal inlet 22″ and ahorizontal outlet 24″ (resembling theinlet 22 andoutlet 24, respectively, but being horizontally oriented) and is thus installable in a horizontal section of a borehole. This embodiment still utilizes the behavior of the low-density fluid rising as a result of its relatively lower density. That is, as the low-density fluid 28 enters theoutlet 24″, the low-density fluid rises into acompartment 30″ (resemblingcompartment 30, but partially formed by awall 50 and being horizontally oriented), as designated byarrows 52. By partially defining thecompartment 30″ with thewall 50 and placing thewall 50 sufficiently far from theoutlet 24″, the low-density fluid 28 will rise into thecompartment 30″ and become trapped well before the low-density fluid reaches theinlet 22″, with thewall 50 secluding or isolating theinlet 22″ from the trapped low-density fluid 28. The flow of injected fluid, as designated again by thearrow 26, will simply flow under the trapped low-density fluid 28 and out theoutlet 24″. - Furthermore, in view of the
trap 14″, it is to be appreciated that while a simple and effective way of secluding the trapped fluid from the inlet of the trap is to create a vertical separation between the compartment and the inlet or pathway leading to the surface (which can be further improved by the use of a check valve, as discussed above), the inlets of the trap and/or debris catch can be located at other locations as well. For example, the inlets and outlets of various embodiments could be placed in the top, bottom, side, or any other desired location of the catch or trap, so long as a compartment is formed that secludes the inlet (with respect to the direction of flow of the injected fluid) of the debris catch and/or fluid trap from the trapped low-density fluid. -
FIG. 8 illustrates a combinedunit 54 including both a low-density fluid trap 14′ and adebris catch 16′″ in a single, integrated assembly. In this embodiment, theline section 12 b would be unnecessary, as the trap and catch are integrated together. The illustrated embodiment of the combinedunit 54 includes abaffle 60, afunnel 62 for thetrap 14′, and afunnel 64 for thecatch 16′″, for directing the low-density fluid 28 into thecompartment 30 and thedebris 32 into thecontainment area 34, respectively. Thebaffle 60 and thefunnel 62 act to seclude or isolate a combinedinlet 66 from the low-density fluid 28 as the low-density fluid 28 migrates up theline 12 c and enters the combinedunit 54 via a combinedoutlet 68, while thebaffle 60 and thefunnel 64 act to contain the debris so it does not clog theinjection line 12. The flow of fluid, as again represented by thearrows 26, flows essentially unimpeded around thebaffle 60 and between the 62 and 64 from thefunnels inlet 66 to theoutlet 68. It is to be appreciated that that features shown could be removed, or replaced or augmented by other features, such as an outlet for venting the compartment, a permeable membrane, screens, a venturi pump, etc. Additionally, the combinedunit 54 could be made rotationally symmetrical, as shown, so that it can be installed in either direction. It is also to be appreciated that, as shown inFIG. 8 , the combinedinlet 66 could be located lower than the combinedoutlet 68 and acheck valve 70 could be included at theinlet 66 or in theline 12 a for creating a chemical fluid barrier, similar to the use of thecheck valve 36 described above, that prevents the migration of the low-density fluid 28 out of thecompartment 30. That is, as the low-density fluid gathers in theunit 54, chemical fluid in theunit 54 will drain down theline 12 c, to reach the level of theoutlet 68. Once the chemical fluid drops down to the level of theoutlet 68, no more chemical fluid will be forced out theoutlet 68 and thecheck valve 70 will prevent back flow out theinlet 66, thereby holding the low-density fluid 28 in theunit 54. - While the invention has been described with reference to an exemplary embodiment or embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt a particular situation or material to the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this invention, but that the invention will include all embodiments falling within the scope of the claims. Also, in the drawings and the description, there have been disclosed exemplary embodiments of the invention and, although specific terms may have been employed, they are unless otherwise stated used in a generic and descriptive sense only and not for purposes of limitation, the scope of the invention therefore not being so limited. Moreover, the use of the terms first, second, etc. do not denote any order or importance, but rather the terms first, second, etc. are used to distinguish one element from another. Furthermore, the use of the terms a, an, etc. do not denote a limitation of quantity, but rather denote the presence of at least one of the referenced item.
Claims (20)
1. A downhole assembly, comprising:
a line operatively arranged to carry a first fluid;
a trap arranged in fluid communication with the line, the trap operatively arranged to enable the first fluid to flow in a first direction, while capturing a second fluid in a compartment, thereby preventing migration of the second fluid through the line in a second direction opposite to the first direction.
2. The assembly of claim 1 , wherein a first density of the first fluid is greater than a second density of the second fluid, and the second fluid rises atop the first fluid into the compartment.
3. The assembly of claim 2 , wherein the first fluid is a liquid and the second fluid is a gas.
4. The assembly of claim 1 , further comprising, with respect to the first direction, an inlet into the trap and an outlet out from the trap, the second fluid entering the trap via the outlet, the compartment operatively arranged to seclude the inlet from the second fluid trapped in the compartment while permitting the first fluid to flow between the inlet and the outlet.
5. The assembly of claim 1 wherein the trap includes a membrane permeable by the second fluid for isolating the compartment from the first fluid.
6. The assembly of claim 5 further comprising a compartment outlet connected to the compartment for releasing the second fluid from the compartment.
7. The assembly of claim 1 , wherein the second fluid is natural gas.
8. The assembly of claim 1 , further comprising a catch fluidly connected to the line, the catch operatively arranged to capture debris while enabling the first fluid to flow therethrough.
9. The assembly of claim 8 , wherein the catch includes a containment area for holding the debris.
10. The assembly of claim 9 , further comprising a baffle, a wall, a funnel, a screen, a cyclone, or combinations including at least one of the foregoing for directing the debris into the containment area or the second fluid into the compartment.
11. The assembly of claim 8 , wherein the trap and the catch are integrated into a single unit having a combined inlet and a combined outlet.
12. The assembly of claim 8 , wherein the catch includes a check valve for preventing back flow of the first fluid or migration of the second fluid up the line.
13. The assembly of claim 12 , wherein the catch is located upstream of the trap with respect to the first direction.
14. The assembly of claim 13 , wherein the trap includes a first inlet and the catch includes a second inlet and the first inlet is positioned higher than the second inlet for creating a vertical separation between the first and second inlets.
15. A method of operating a downhole system, comprising:
injecting a first fluid through a line in a first direction; and
capturing a second fluid in a compartment connected in fluid communication with the line, the second fluid traveling through the line in a second direction opposite to the first direction.
16. The method of claim 15 , wherein a first density of the first fluid is greater than a second density of the second fluid and the second fluid rises atop the first fluid into the compartment.
17. The method of claim 15 , further comprising pumping the second fluid out of the compartment via an outlet connected to the compartment.
18. The method of claim 17 , wherein the outlet is separated from the first fluid via a membrane, the second fluid permeable through the membrane.
19. The method of claim 15 , further comprising capturing debris traveling down the line in a debris catch, the debris catch in fluid communication with the line.
20. The method of claim 19 , wherein the debris catch is arranged at a vertically lower position than the compartment and located upstream of the compartment with respect to the first direction of flow.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/530,369 US20120325468A1 (en) | 2011-06-24 | 2012-06-22 | Fluid migration shut-off |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201161500995P | 2011-06-24 | 2011-06-24 | |
| US13/530,369 US20120325468A1 (en) | 2011-06-24 | 2012-06-22 | Fluid migration shut-off |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20120325468A1 true US20120325468A1 (en) | 2012-12-27 |
Family
ID=47360737
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13/530,369 Abandoned US20120325468A1 (en) | 2011-06-24 | 2012-06-22 | Fluid migration shut-off |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20120325468A1 (en) |
| WO (1) | WO2012178041A2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015047955A1 (en) * | 2013-09-24 | 2015-04-02 | Baker Hughes Incorporated | Subterranean solids separator |
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| US6623640B2 (en) * | 1999-09-28 | 2003-09-23 | Biothane Corporation | Phase separator having multiple separation units, upflow reactor apparatus, and methods for phase separation |
| US20050145388A1 (en) * | 2002-04-08 | 2005-07-07 | Hopper Hans P. | Subsea process assembly |
| US20090288818A1 (en) * | 2008-05-22 | 2009-11-26 | Bak | Passive gas separator for progressing cavity pumps |
| US7905946B1 (en) * | 2008-08-12 | 2011-03-15 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Systems and methods for separating a multiphase fluid |
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| US4424068A (en) * | 1982-12-06 | 1984-01-03 | Mcmillan John F | Separator and method for separation of oil, gas and water |
| US5025762A (en) * | 1989-08-01 | 1991-06-25 | Sanshin Kogyo Kabushiki Kaisha | Two cycle engine for small boat |
| GB9727078D0 (en) * | 1997-12-23 | 1998-02-18 | Univ Sheffield | Fluidic level control systems |
| NO339387B1 (en) * | 2008-04-23 | 2016-12-05 | Vetco Gray Inc | Water separator system for use in well operations |
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2012
- 2012-06-22 WO PCT/US2012/043792 patent/WO2012178041A2/en active Application Filing
- 2012-06-22 US US13/530,369 patent/US20120325468A1/en not_active Abandoned
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5904850A (en) * | 1995-04-10 | 1999-05-18 | Paques B.V. | Settling device for a fluid containing liquid, gas and particulate material, as well as a cleaning device provided herewith and a method for cleaning waste water |
| US6623640B2 (en) * | 1999-09-28 | 2003-09-23 | Biothane Corporation | Phase separator having multiple separation units, upflow reactor apparatus, and methods for phase separation |
| US6228146B1 (en) * | 2000-03-03 | 2001-05-08 | Don R. Kuespert | Gas recovery device |
| US20030051874A1 (en) * | 2001-09-20 | 2003-03-20 | Munson Curtis L. | Downhole membrane separation system with sweep gas |
| US20050145388A1 (en) * | 2002-04-08 | 2005-07-07 | Hopper Hans P. | Subsea process assembly |
| US20090288818A1 (en) * | 2008-05-22 | 2009-11-26 | Bak | Passive gas separator for progressing cavity pumps |
| US7905946B1 (en) * | 2008-08-12 | 2011-03-15 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Systems and methods for separating a multiphase fluid |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2015047955A1 (en) * | 2013-09-24 | 2015-04-02 | Baker Hughes Incorporated | Subterranean solids separator |
| GB2534515A (en) * | 2013-09-24 | 2016-07-27 | Baker Hughes Inc | Subterranean solids separator |
| US9494005B2 (en) | 2013-09-24 | 2016-11-15 | Baker Hughes Incorporated | Subterranean solids separator |
| GB2534515B (en) * | 2013-09-24 | 2020-05-27 | Baker Hughes Inc | Subterranean solids separator |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2012178041A3 (en) | 2013-03-14 |
| WO2012178041A2 (en) | 2012-12-27 |
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